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US4392003A Expired / Lapsed US ⏱️ 0.0 years remaining

Isobutene by dehydroisomerization of normal butane

Assignee: BP PLC
•
Filing: 1981-06-08
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Granted: 1983-07-05
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Expires: 2001-06-08
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Abstract

Abstract This invention relates to a method of dehydroisomerizing n-butane by contacting at elevated temperatures a feedstock containing n-butanes with a catalyst composition containing a gallium compound on a support. The process affords a valuable method of producing iso-butene which is a basic chemical feedstock for a number of products including polyisobutenes, methacrolein and methyl tertiary butyl ether, to name a few. The last named compound can be prepared by reacting isobutene with methanol and is a convenient means of separating iso-butene from the products of the dehydroisomerization stage.

Inventors

  • 👤 Alexander J. Kolombos
  • 👤 Clive D. Telford
  • 👤 Dennis Young

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 08:17
CPC Classifications
C; C07; C07C; C07C11/00; C07C11/02; C07C11/08; C07C11/09; C07C5/00; C07C5/32; C07C5/373

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 76 words
A process for dehydroisomerisation of a hydrocarbon feedstock containing normal butane to isobutene which comprises bringing the feedstock at an elevated temperature into contact in a single stage with a catalyst composition comprising an element from Group IIIa of the Periodic Table or a compound thereof in combination with a support of α-value below 45, said support being a zeolite selected from the group consisting of an aluminosilicate, a silicalite, a metal tectosilicate, and a boralite.
Claim 2
Dependent Claim 76 words
A process for dehydroisomerisation of a hydrocarbon feedstock containing normal butane to isobutene which comprises bringing the feedstock at an elevated temperature into contact in a single stage with a catalyst composition comprising an element from Group IIIa of the Periodic Table or a compound thereof in combination with a support of α-value below 45, said support being a zeolite selected from the group consisting of an aluminosilicate, a silicalite, a metal tectosilicate, and a boralite.
Claim 3
Dependent Claim 15 words
A process according to claim 1 wherein a gallium compound is deposited on a support.
Claim 4
Dependent Claim 13 words
A process according to claim 2 wherein the gallium compound is gallium oxide.
Claim 5
Dependent Claim 20 words
A process according to claim 1 wherein gallium ions from a gallium compound are exchanged with cations on the support.
Claim 6
Dependent Claim 29 words
A process according to claims 1, 2, 3, or 4 wherein the concentration of gallium in the catalyst composition is between 0.05 and 20% by weight of the support.
Claim 7
Dependent Claim 39 words
A process according to preceding claims 1, 2, 3, or 4 wherein the dehydroisomerisation reaction is carried out by passing the feedstock in the vapour phase over the catalyst composition maintained at a temperature between 350° and 700° C.
Claim 8
Dependent Claim 28 words
A process according to claims 1, 2, 3, or 4 wherein the isobutene formed is separated from the dehydroisomerisation reaction products by conversion thereof into methyl tertiarybutyl ether.
Claim 9
Dependent Claim 22 words
A process according to claim 7 wherein the conversion to methyl tertiarybutyl ether is achieved by reacting the dehydroisomerisation products with methanol.

References Cited (Backward Citations)

CA737533A Cited
US2389406A Cited
US3804746A Cited
US4056576A Cited
GB1507549A Cited
US4329516A Cited
EP0024930A1 Cited
US4304686A Cited
US4324940A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-07-04 1987-01-03 1987-07-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-07-04 1991-01-03 1991-07-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-07-04 1995-01-03 1995-07-05 $7700.00 Window Closed / Lapsed

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